WO2013016414A1 - Processing of dielectric fluids with mobile charge carriers - Google Patents
Processing of dielectric fluids with mobile charge carriers Download PDFInfo
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- WO2013016414A1 WO2013016414A1 PCT/US2012/048128 US2012048128W WO2013016414A1 WO 2013016414 A1 WO2013016414 A1 WO 2013016414A1 US 2012048128 W US2012048128 W US 2012048128W WO 2013016414 A1 WO2013016414 A1 WO 2013016414A1
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- charge carriers
- dielectric fluid
- mobile charge
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- discharges
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G32/00—Refining of hydrocarbon oils by electric or magnetic means, by irradiation, or by using microorganisms
- C10G32/02—Refining of hydrocarbon oils by electric or magnetic means, by irradiation, or by using microorganisms by electric or magnetic means
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G15/00—Cracking of hydrocarbon oils by electric means, electromagnetic or mechanical vibrations, by particle radiation or with gases superheated in electric arcs
- C10G15/08—Cracking of hydrocarbon oils by electric means, electromagnetic or mechanical vibrations, by particle radiation or with gases superheated in electric arcs by electric means or by electromagnetic or mechanical vibrations
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/08—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for compression ignition
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B3/00—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties
- H01B3/18—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances
- H01B3/20—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances liquids, e.g. oils
- H01B3/22—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances liquids, e.g. oils hydrocarbons
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
- C10G2300/1007—Used oils
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1011—Biomass
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1055—Diesel having a boiling range of about 230 - 330 °C
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/302—Viscosity
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2250/00—Structural features of fuel components or fuel compositions, either in solid, liquid or gaseous state
- C10L2250/08—Emulsion details
- C10L2250/084—Water in oil (w/o) emulsion
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/38—Applying an electric field or inclusion of electrodes in the apparatus
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
Definitions
- the method can further refine the fluids and/or improve the viscosity and flowability of the fluids.
- the API gravity of the oils in these deposits typically ranges from 10° to 6° in the Athabasca sands in Canada to even lower values in the San Miguel sands in Texas, indicating that the oil is highly viscous in nature.
- a problem of heavy oil is that it takes large amounts of thermal energy and expensive catalysts to upgrade, in addition to the transportation costs. Therefore, new technologies are being sought for several reasons: 1) implementation in the refinery at lower temperatures 2) less sensitivity to oil contaminants 3) implementation prior to transportation, either, down-hole or at the well head rather than in the refinery, as this will lower transportation costs.
- Thermal cracking is the process in which long hydrocarbon chains (heavy hydrocarbons) are broken into shorter simpler molecules (light hydrocarbons). It occurs through the breaking of carbon-carbon bonds in the original molecule. Typically this is done with temperature and catalysts. Done in the presence of hydrogen this is called hydrotreating and results in saturated hydrocarbons such as alkanes and naphthenes. Done with steam in short residence time reactors (hydrocracking) this process is used to treat heavier hydrocarbons to produce ethylene, at high temperatures ( ⁇ 900°C), or liquid hydrocarbons for use in gasoline or fuel oil, at lower temperatures. In cracking various chains of reactions takes place initiated by the formation of a radical as shown in Table 1 for a simple hydrocarbon (though similar processes occur for longer hydrocarbons). A single initiation reaction may feed several additional, decomposition abstraction reactions before terminating.
- 'Non-Thermal' or 'cold plasma' cracking is generally similar to thermal cracking except that the initiation reaction occurs due to impact with a plasma produced species such as an electron, ion, photon, or electrically or vibrationally excited state which is not in equilibrium with the bulk of the matter being treated.
- a plasma produced species such as an electron, ion, photon, or electrically or vibrationally excited state which is not in equilibrium with the bulk of the matter being treated.
- the plasma treatment of gaseous hydrocarbons or vaporized liquid fuels is well known.
- the non-equilibrium nature of the plasma allow for significantly more efficient and rapid chemical reactions than an equilibrium system at similar temperature.
- the chemical reaction pathways in a non-thermal plasma can be more numerous than in a equilibrium system.
- Significantly less research has been done on the direct upgrading of liquid fuels using nonthermal plasma methods of hydrocarbon cracking.
- Plasma discharges submerged in liquids are a subset of plasma liquid interactions which more generally include other systems such as discharges near liquid surfaces, discharges in gases with aerosolized droplets and discharges onto a liquid surface.
- submerged plasma discharge systems are well known, consisting of electrodes submerged in a liquid, and may either generate a plasma from gas bubble injected into the liquid or through the dielectric breakdown of the liquid potentially with bubble formation but without bubble addition.
- they consist of discharge between two stationary electrodes connected to an external circuit.
- the discharges in such systems are generally very non-uniform and most such systems have very high energy released (on the order of Joules) during the discharge process.
- the dielectric fluid is a hydrocarbon fluid such as a heavy crude oil or a fuel.
- the charge carrier comprises water droplets.
- the mobile charge carriers are metallic balls. In both instances the discharges initiate from the mobile charge carriers.
- the present invention is based upon the discovery that the use of mobile charge carriers within the dielectric fluid, whether the charge carriers are pre-existing in the fluid or added, and applying an electric field thereto allows one to initiate a chemical reaction within the dielectric fluid in a very controlled manner.
- the chemical reaction is initiated by plasma discharges enabled by the presence of the mobile charge carriers.
- the energy released in the plasma discharges are very controllable due to the small and controllable capacitance of the mobile charge carriers, control of the electric circuit, and control of the materials properties of the charge carrier. Controlling the energy release in the discharges allows for control of the state of the plasma and temperature which is generated in the discharge which further allows fine tunability as to the chemical reaction that takes place.
- the dielectric fluid can therefore be processed in a low temperature process employing highly non-equilibrium discharges.
- Fig. 1 of the drawing shows an image of plasma discharges between water droplets in oil. Mineral oil and blue dyed water droplets are used for visualization.
- Fig. 2 shows a schematic of an oil treatment reactor.
- Fig. 3 graphically depicts the viscosity of a treated mixture at 26°C as a function of various input powers tested.
- FIG. 4 schematic of another embodiment of an oil treatment reactor
- the present invention employs mobile discharge carriers within a dielectric fluid to create plasma discharges within the dielectric fluid.
- the discharge creates radicals which initiate a chemical reaction.
- the type and extent of the chemical reaction can be controlled through the control of the energy release in the discharges.
- the discharges within the dielectric fluid can be controlled by the types of mobile charge carriers used.
- the material and size of the carriers will dictate the energy release in the discharges.
- the capacitance of the mobile charge carriers and the charge transferred to the mobile carrier during collisions helps to control and dictate the energy release.
- hydrocarbon The discharges generated are very small with typical sizes 2 um to 100 um. There is a high surface to volume ratio for the plasma and liquid and the plasma is generated from species present in the liquid. For the discharge in the liquid or fluid, almost every radical generated in the plasma system with the mobile charge carriers interacts with molecules from the liquid phase.
- the dielectric fluid can be any dielectric fluid, non-conducting (or poorly conducting) fluid, which can be in need of processing.
- the dielectric fluid is a hydrocarbon containing fluid.
- the hydrocarbon fluid can be a heavy crude oil, gasoline or diesel fuel.
- the fluid can also be a bio fuel liquid or other alternative or non-traditional fuels.
- the mobile charge carriers are within the dielectric fluid so that the discharges emanate in the fluid and are distributed throughout the fluid. The mobile charge carriers move within the dielectric fluid, generally bouncing between the two electrodes, or colliding with one another. Discharges are generally initiated upon these collisions.
- the size of the mobile charge carriers can vary as needed. Changing the size and shape of the carrier changes the capacitance of the carrier and thus the stored energy on the charge carrier. Carrier size is thus a method to easily control the energy released during the plasma discharge.
- the mobile charge carriers can comprise metal filings, water bubbles or spherical balls.
- the metal filings can be any shape, e.g., a cylindrical or of a branched shape.
- the filings can be made of a metal such as steel, aluminum or brass.
- the spherical balls can also be made of materials such as steel, aluminum or brass. Also, the spherical balls can be made of a material such as a ceramic material, as long as the material is of a different dielectric constant than the dielectric fluid so it can carry a charge.
- the dielectric fluid can be processed using a batch reactor as shown in Fig. 2.
- the dielectric fluid can also flow between two electrodes.
- the charge carriers can flow with the dielectric fluid, or, the charge carriers can be stationary, between the electrodes, with the dielectric fluid passing over the charge carriers.
- a water in oil emulsion is preexisting or created by the addition of water to oil or oil to a water-oil emulsion.
- the water is an electrolyte with conductivity greater than approximately 0.1 mS/cm. Appropriate conductivity is most likely inherent in the produced oil-water emulsion but could be created by the addition of salts.
- the water exists as bubbles ranging in size from microscopic ( ⁇ 50 ⁇ ) to several millimeters in diameter.
- the oil-water emulsion is placed between two electrodes and an electric field in the range of 1 to 100 kV/cm is applied. In such conditions the water droplets bounce between the electrodes as charge carriers.
- the water droplets deform under electrophoretic forces and form sharp microscopic charged surfaces which may generate short duration plasma discharges in between the bubbles and at bubble-electrode interfaces, as shown in Figure 1.
- other conducting particles or liquids added to or preexisting in the emulsion can act as charge carriers and promote discharges and the chemical and physical treatment of the oil.
- the electrical discharge and processing of the fluid e.g., oil, can be controlled.
- the discharge energies can be controlled to levels an order of magnitude below the mJ level.
- the energy released in the discharge has an energy of between InJ and lOmJ.
- the discharge has an energy of ⁇ ⁇ and lOmJ, and in another embodiment an energy between ⁇ ⁇ ] and ⁇ In another embodiment the discharge has an energy of between InJ and 1 ⁇
- External circuit control The discharge between the charge carriers can be sporadic in nature or occur at a repeatable frequency depending on the geometry of the electrodes and reactor. In both such situations the stored energy on the charge carrier accessible from the external circuit, can cause intense or weak discharges to be generated. Energy stored in capacitors in the external circuit can be released to the charge carriers slowly through ballast resistors and inductors or rapidly.
- the amount of energy release can similarly be controlled by the size of the external capacitor.
- the rate of and amount of energy release will affect the temperature, duration, and intensity of the discharge charge, shock waves and light emission. Slow current release was observed to actually form near continuous discharges inside of formed gas bubbles between the charge carriers and electrodes.. Faster and lower energy releases lead to nanosecond duration discharges with only on the order of micro-Joules of energy released. ii. Number or charge carriers and charge carrier interactions - the number of charge carriers will affect whether carrier-electrode or carrier-carrier collision are more prevalent. As each type of collision has a different energy release the predominance of certain chemical pathways over others could be controlled.
- the multiple charge carriers can also be of various size and material further adjusting the energy release profiles.
- the mobile charge carriers can be free to interact with one another, as in Figure 2, or can be individually confined so that there only one charge carrier between each electrode and collisions are only with the electrodes.
- the charge carriers can be controlled to self-organize into chains, as in Figure 1 , or randomly distribute as in Figure 2.
- Additives - chemically reacting species and surfaces can be added to the system for example: a) Gases can be bubbled through the liquid - for example 3 ⁇ 4 or C3 ⁇ 4 and can act as hydrogen donors to help hydrogenate the hydrocarbons. Gas bubbles are also produced during the discharges.
- Hydrogen donors can be added to the oil - for example Tetralin has been used as a hydrogen donor.
- the hydrogen donor functions to supply hydrogen to thermally cracked hydrocarbon fragments to thereby reduce coke formation and provide a superior cracked product.
- Hydrogen donors can be added as water or within the water (for example ammonia (NH 3 , up to 4%) is easily added to the water and in initial experiments did not change the discharge behavior, yet may provide additional hydrogenation.
- ammonia NH 3 , up to 48% is easily added to the water and in initial experiments did not change the discharge behavior, yet may provide additional hydrogenation.
- Acidic solutions - the use of acidic solutions should provide H + ions for potential reactions in a manner similar to how acidic solid catalyst are used in hydrocracking.
- Solid particle addition - metallic particle (as in Figure 2) of various size or metallic catalyst particle (Pt for example) can be mixed in the oil instead of or in addition to water droplet to promote reactions or change the discharge conditions.
- Pressure and temperature variations can be employed to effect the desired reaction.
- the oil may be operated hot to increase the thermal energy available for reactions or at varying pressure to change the equilibrium conditions, rate of chemical reactions, and bubble growth rates.
- the Boscan crude was mixed with mineral oil as a diluting agent to reduce the viscosity during treatment and also as a relatively low cost saturated hydrocarbon mixture that can serve as a hydrogen donor.
- the mixture was approximately a 70% / 30% mass ratio (later sim-dist analysis indicates it may be closer to 68.3%, 31.2%) the same large batch mixture was used to for the treated and untreated sample.
- the untreated mixture had a viscosity of 3.5 Pa-s (3500 cP) at room temperature (26°C).
- Three sample volumes of about 25 mL ( ⁇ 24 g) were treated using a plasma discharge process in the oil. Up to 40% reductions in viscosity were measured at the highest energies tested see Table 1.
- Figure 3 shows the viscosity reduction as a function of input power.
- the reactor used is shown in Figure 2.
- An unballasted high voltage power supply applied up to 20 kV across the oil filled discharge gap.
- the inter electrode spacing is about 2 cm.
- the metal balls charge when in contact with the electrodes.
- the metal balls move acting as charge carriers between the electrodes and creating microplasmas when they collide with each other or with the electrodes.
- various current discharges (5 uA to 5 mA) are possible.
- Discharges are initiated when conducting particles gain charge at an electrode immersed in the oil and then collide with one another.
- the electric field between two particles of different charge is sufficient to initiate an electric discharge.
- the interesting electrodynamics of this system provide a controllable method for the chemically processing of liquids.
- the microdischarge and spark chains types are shown for water in Fig. 1.
- the gas bubble charges occur when a high ballast resistance is used and with more viscous fluids and entails the formation of a discharge within a gas bubble between two charge carriers. This occurs because the discharge is stabilized by the ballasting and the gas bubble is more stable due to the high fluid viscosity.
- the microspark discharges are very short in duration and low in energy and occur between isolated charge carriers during collisions when there is more chaotic particle motion, and for higher electric fields.
- spark chains occur when the charged particles self organize into chains and higher energy sparks carry current from one electrode to the other.
- Table 2 show a analysis of the GC traces of the helium ionization detector (HID) attained for gas sampled from the reactor at the low voltage (low energy per pulse) and high voltage (high energy per pulse) operating conditions.
- Identified hydrocarbon peaks are labeled 1-8.
- the peaks are identified as 1 : hydrogen, 2: methane, 3: overlapping acetylene and ethylene, and 4: ethane. Peaks 5 and 6 are not specifically identified C 3 s and peaks 7 and 8 are similarly C 4 s.
- Lower energy/pulse discharges produced lower concentration of hydrogen and methane while producing relatively higher concentrations of higher hydrocarbons C 2 , C 3 and C 4 .
- Case 1 would be more desirable for hydrogen generation for polymer membrane fuel cells.
- Case 2 would be more desirable for high energy density compressible fuels for solid oxide fuel cells.
- Case 2 would be more desirable for the conversion of the JP8 to gasoline.
- FIG. 4 To process larger amounts of fuel in a more controlled manner an embodiment of this technology as shown in figure 4 was built.
- This reactor consisted of 300 bouncing balls between electrodes operated in parallel. In this geometry on charge carrier to electrode collisions are allowed.
- a detailed CAM drawing and photo of the reactor is shown in Figure 4.
- a 10x10 array of vertical columns with intersecting lateral holes for gas venting and electrode feed troughs was fabricated from nylon using a prototyping machine. The electrode wires were alternated vertically giving two ground electrode planes and two high voltage planes and allow for three layers of balls to operate in each column, as shown in figure 4. This geometric configuration could be scaled up to every larger scale.
- the system is operated using a single unballasted DC power supply at voltages between 10 kV and about 18 kV and corresponding currents of 0.05 mA to 0.2 mA. An individual ball would bounce at a frequency of about 60 to 130 Hz over this range. Corresponding discharge energies per microplasma were 28 uJ and 92 ⁇ per pulse at the low and high voltage operation.
- the reactor was operated inside of a pressure sealed reaction chamber and immersed in JP8. The gas was sampled for GC analysis.
- the present invention can provide a low temperature, controllable method of processing, further refining dielectric fluids. Particular applicability can be found with further refining hydrocarbon fluids, which can occur at the wellhead, in the wellbore, or in a refinery.
- the reactions can involve hydrocracking in order to improve the viscosity and flowability of the fluid.
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Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
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CA2842694A CA2842694A1 (en) | 2011-07-25 | 2012-07-25 | Processing of dielectric fluids with mobile charge carriers |
BR112014001862A BR112014001862A2 (en) | 2011-07-25 | 2012-07-25 | dielectric fluid processing with mobile load chargers |
CN201280036729.3A CN103765526A (en) | 2011-07-25 | 2012-07-25 | Processing of dielectric fluids with mobile charge carriers |
RU2014106829/04A RU2014106829A (en) | 2011-07-25 | 2012-07-25 | PROCESSING DIELECTRIC FLUIDS WITH MOBILE CHARGE CARRIERS |
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US201161511297P | 2011-07-25 | 2011-07-25 | |
US61/511,297 | 2011-07-25 | ||
US13/556,739 US9228136B2 (en) | 2011-07-25 | 2012-07-24 | Processing of dielectric fluids with mobile charge carriers |
US13/556,739 | 2012-07-24 |
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WO2013016414A1 true WO2013016414A1 (en) | 2013-01-31 |
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US (1) | US9228136B2 (en) |
CN (1) | CN103765526A (en) |
BR (1) | BR112014001862A2 (en) |
CA (1) | CA2842694A1 (en) |
RU (1) | RU2014106829A (en) |
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US10627990B2 (en) | 2013-09-13 | 2020-04-21 | Ntt Docomo, Inc. | Map information display device, map information display method, and map information display program |
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US9806639B2 (en) * | 2015-04-29 | 2017-10-31 | General Electric Company | Dielectric fluids for linear switched capacitive devices |
EP3781649A4 (en) * | 2018-04-20 | 2021-12-15 | The Texas A&M University System | Process for partial upgrading of heavy oil |
US11193513B2 (en) | 2018-07-18 | 2021-12-07 | The Texas A&M University System | Efficient mechanical generation of cavitation in liquids |
US11404976B2 (en) * | 2019-09-06 | 2022-08-02 | Wisconsin Alumni Research Foundation | Dielectric nano-fluid for electrostatic machines and actuators |
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- 2012-07-25 BR BR112014001862A patent/BR112014001862A2/en not_active IP Right Cessation
- 2012-07-25 CA CA2842694A patent/CA2842694A1/en not_active Abandoned
- 2012-07-25 RU RU2014106829/04A patent/RU2014106829A/en unknown
- 2012-07-25 CN CN201280036729.3A patent/CN103765526A/en active Pending
- 2012-07-25 WO PCT/US2012/048128 patent/WO2013016414A1/en active Application Filing
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US4223241A (en) * | 1978-08-28 | 1980-09-16 | The United States Of America As Represented By The Secretary Of The Navy | Electrostatic charge generator |
US5332529A (en) * | 1992-03-05 | 1994-07-26 | Texaco Inc. | Electric discharge machine process and fluid |
WO2002077194A2 (en) * | 2001-03-26 | 2002-10-03 | Linden Technologies, Inc. | Polymer synthesis |
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US20130161232A1 (en) | 2013-06-27 |
CN103765526A (en) | 2014-04-30 |
US9228136B2 (en) | 2016-01-05 |
RU2014106829A (en) | 2015-08-27 |
CA2842694A1 (en) | 2013-01-31 |
BR112014001862A2 (en) | 2017-02-21 |
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